US4487740A - Procedure and equipment for injecting gas into liquids - Google Patents
Procedure and equipment for injecting gas into liquids Download PDFInfo
- Publication number
- US4487740A US4487740A US05/947,671 US94767178A US4487740A US 4487740 A US4487740 A US 4487740A US 94767178 A US94767178 A US 94767178A US 4487740 A US4487740 A US 4487740A
- Authority
- US
- United States
- Prior art keywords
- gas
- nozzles
- bubble column
- group
- conduit
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Classifications
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21C—NUCLEAR REACTORS
- G21C15/00—Cooling arrangements within the pressure vessel containing the core; Selection of specific coolants
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/232—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
- B01F23/2322—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles using columns, e.g. multi-staged columns
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E30/00—Energy generation of nuclear origin
- Y02E30/30—Nuclear fission reactors
Definitions
- This invention is directed to a procedure for injecting gas into liquids, and, more particularly to the injection of hydrogen into the primary coolant of pressurized water nuclear power plants.
- the makeup tank is used to equalize primary coolant volume changes, and contains both the primary coolant and a hydrogen-gas blanket.
- the problem is solved in that the liquid flows through a bubble column, only the gas volume necessary for reaching the required gas content is injected into the bubble column above the liquid inlet, and the gas and liquid are mixed prior to leaving the bubble column.
- the device used for implementing this procedure has a bubble column that contains several motionless mixers.
- the gas feed line is equipped with a gas pump, and the pipe section of the two-conduit gas injection line arranged inside the bubble column is equipped with nozzles.
- the nozzles moreover, can be flushed with the aid of a bypass flow of the liquid to be gassed.
- An advantage of this feature is that the bypass flow conduits are connected with the pipe sections that support the nozzles.
- a ventilation line is also attached at the bubble column in order to prevent gas bubble formation in the primary coolant.
- Analyses measuring devices are installed in the liquid line upstream and downstream of the bubble column.
- the gas volume injected through the gas pump depends upon the pre-existing hydrogen concentration of the liquid to be injected with gas, and the head of the liquid flow.
- the isolation valves of the bypass flow conduits can be manipulated to enable the nozzles to be covered with gas and rinse water on alternate sides.
- conduit 14 the primary coolant to be injected with gas flows into a pressurized water reactor system (not shown) in the direction of arrow 19, and after the adjustment of the volume flow control valve 10, flows into bubble column 6 at liquid inlet 20.
- gas proportioning or dosage equipment e.g. gas dosage pump 1
- the hydrogen gas in conduit 2 is channeled into the bubble column 6 and is injected above liquid inlet 20 via the double gas injection conduits 2a or 2b, and nozzles 5 or 5a.
- the mode of operation for implementing the flushing process enables the nozzles 5, 5a to be flushed alternately, or to be used for gas injection.
- isolation valves 3 and 11a are closed and isolation valves 11 and 3a are open.
- isolation valves 3a and 11 are closed and isolation valves 11a and 3 are open.
- Check valves 4a, 12a, 4 and 12 prevent gas or flushing liquid from returning.
- An analysis measuring device 8 is installed in bypass conduit 13, which measures the hydrogen gas concentration of the liquid to be injected with gas so that exact gas dosing can be accomplished through the gas dosage pump 1 as a function of gas content and liquid volume in conduit 14.
- Nitrogen moreover, can be used as a gas blanket for the makeup tank, in order to avoid the danger of a combustible gas explosion.
- An additional advantage of the invention is the fact that the hydrogen concentration of the reinjected primary coolant can be kept within a specified range during load change processes.
Landscapes
- Physics & Mathematics (AREA)
- Engineering & Computer Science (AREA)
- High Energy & Nuclear Physics (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Plasma & Fusion (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Monitoring And Testing Of Nuclear Reactors (AREA)
- Accessories For Mixers (AREA)
- Measuring Volume Flow (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Geophysics And Detection Of Objects (AREA)
- Preventing Corrosion Or Incrustation Of Metals (AREA)
Abstract
A method and apparatus is shown for establishing a predetermined concentration of gas in the reactor core coolant for a pressurized water nuclear power system. Gas is added to core coolant water in a bubble column. The gas-water mixture flows through static mixers in the column to produce the desired gas concentration in the water.
Description
This invention is directed to a procedure for injecting gas into liquids, and, more particularly to the injection of hydrogen into the primary coolant of pressurized water nuclear power plants.
For example, it is not uncommon in nuclear power plants, to inject hydrogen gas into primary coolant water by spraying the primary coolant into an hydrogen atmosphere, e.g. into the hydrogen gas blanket of the makeup tank, or by bubbling hydrogen gas in the water phase of the makeup tank. The makeup tank among other things, is used to equalize primary coolant volume changes, and contains both the primary coolant and a hydrogen-gas blanket.
These known procedures have the disadvantage that due to the large hydrogen volume in the makeup tank, a release of relatively large hydrogen volumes into the space surrounding the makeup tanks is possible, and therefore the occurrence of combustible gas explosions must be taken into account. Further, the gas/water concentration can not be precisely controlled.
There is a need, therefore, to find a procedure through which a predetermined gas concentration can be reached in the liquid under consideration and through which the potential release of dangerous volumes of explosive gas can be minimized.
The problem is solved in that the liquid flows through a bubble column, only the gas volume necessary for reaching the required gas content is injected into the bubble column above the liquid inlet, and the gas and liquid are mixed prior to leaving the bubble column.
The device used for implementing this procedure has a bubble column that contains several motionless mixers. The gas feed line is equipped with a gas pump, and the pipe section of the two-conduit gas injection line arranged inside the bubble column is equipped with nozzles.
The nozzles, moreover, can be flushed with the aid of a bypass flow of the liquid to be gassed. An advantage of this feature is that the bypass flow conduits are connected with the pipe sections that support the nozzles.
A ventilation line is also attached at the bubble column in order to prevent gas bubble formation in the primary coolant. Analyses measuring devices are installed in the liquid line upstream and downstream of the bubble column.
The gas volume injected through the gas pump depends upon the pre-existing hydrogen concentration of the liquid to be injected with gas, and the head of the liquid flow.
In accordance with a specific embodiment of the invention, the isolation valves of the bypass flow conduits can be manipulated to enable the nozzles to be covered with gas and rinse water on alternate sides.
The method and apparatus for implementing the invention are shown in a schematic drawing.
In conduit 14 the primary coolant to be injected with gas flows into a pressurized water reactor system (not shown) in the direction of arrow 19, and after the adjustment of the volume flow control valve 10, flows into bubble column 6 at liquid inlet 20. With the aid of gas proportioning or dosage equipment, e.g. gas dosage pump 1, the hydrogen gas in conduit 2 is channeled into the bubble column 6 and is injected above liquid inlet 20 via the double gas injection conduits 2a or 2b, and nozzles 5 or 5a.
Hydrogen gas and primary coolant are now intensively mixed when liquid flows through motionless mixer 7. After the liquid has flowed through the mixer 7, the primary coolant which has been provided with the desired hydrogen content, discharges from the bubble column 6 through conduit 15. Automatic ventilation through the conduit 16, float valve 17 and isolation valve 18 ensures that no gas bubbles remain in the primary coolant. Bypass conduit 13 in which coolant flows in the direction of arrow 21, which comprises a certain portion of the primary coolant that to be injected with gas flows, branches off from the conduit 14.
The mode of operation for implementing the flushing process enables the nozzles 5, 5a to be flushed alternately, or to be used for gas injection. For the case "flush nozzle 5", isolation valves 3 and 11a are closed and isolation valves 11 and 3a are open. For the case "flush nozzle 5a" isolation valves 3a and 11 are closed and isolation valves 11a and 3 are open. Check valves 4a, 12a, 4 and 12 prevent gas or flushing liquid from returning.
An analysis measuring device 8 is installed in bypass conduit 13, which measures the hydrogen gas concentration of the liquid to be injected with gas so that exact gas dosing can be accomplished through the gas dosage pump 1 as a function of gas content and liquid volume in conduit 14.
It should also be noted that the entire gassing and flushing process takes place automatically.
Gassing in accordance with the principles of the invention now is possible in a simplified and advantageous manner. Nitrogen, moreover, can be used as a gas blanket for the makeup tank, in order to avoid the danger of a combustible gas explosion.
An additional advantage of the invention is the fact that the hydrogen concentration of the reinjected primary coolant can be kept within a specified range during load change processes.
Claims (5)
1. A device for injecting a gas into a stream of reactor coolant for a pressurized water nuclear power plant comprising:
a bubble column, the stream of reactor coolant being directed up therethrough;
motionless mixer means positioned within said bubble column for mixing the stream of reactor coolant;
a gas pump;
gas conduit means for establishing fluid communication between said gas pump and said bubble column below said motionless mixer means;
a plurality of nozzles on said gas conduit means establishing fluid communication between said gas conduit means and the stream of reactor coolant within said bubble column;
gas analysis measuring apparatus for measuring the gas concentration in the reactor coolant liquid.
2. A device as in claim 1 further comprising:
by-pass flow conduit means for establishing fluid communication between the coolant prior to entry into said bubble column and said plurality of nozzles to enable a portion of the stream of reactor coolant to bypass a portion of said bubble column and flush a portion of said plurality of nozzles;
valve means for selectively isolating said plurality of nozzles from said gas injection conduit means and said by-pass flow conduit means.
3. A device as in claim 2 wherein:
said plurality of nozzles include a first group of nozzles and a second group of nozzles;
said gas conduit means includes a first gas conduit and a second gas conduit establishing fluid communication between said first group of nozzles and said second group of nozzles respectively;
said by-pass flow conduit means including a first by-pass flow conduit and a second by-pass flow conduit providing fluid communication between the coolant prior to entry into said bubble column and said first group of nozzles and said second group of nozzles respectively;
said valve means being capable of selectively isolating said first group of nozzles and said second group of nozzles from said gas pump while by-pass flow is directed therethrough, while said second group of nozzles and said first group of nozzles respectively remain in fluid communication with said gas pump to provide flushing without interrupting the gas injection.
4. A device according to claim 1 further comprising:
a vent conduit to eliminate gas bubbles from the reactor coolant liquid in said bubble column above said motionless mixer means; and, vent valve means for isolating said vent conduit and precluding backflow through said vent conduit into said bubble column.
5. A method for injecting gas into a reactor coolant for a pressurized water nuclear power plants comprising the steps of passing the coolant up through a bubble column that has a liquid inlet, injecting only the gas quantity needed for reaching a predetermined gas concentration in the coolant into the bubble column above the liquid inlet and mixing the gas and the coolant prior to leaving the bubble column.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE2748159 | 1977-10-27 | ||
| DE2748159A DE2748159C2 (en) | 1977-10-27 | 1977-10-27 | Device for gassing the primary coolant of a water-cooled nuclear reactor plant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US4487740A true US4487740A (en) | 1984-12-11 |
Family
ID=6022389
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US05/947,671 Expired - Lifetime US4487740A (en) | 1977-10-27 | 1978-10-02 | Procedure and equipment for injecting gas into liquids |
Country Status (11)
| Country | Link |
|---|---|
| US (1) | US4487740A (en) |
| EP (1) | EP0001903B1 (en) |
| JP (1) | JPS5923398B2 (en) |
| AT (1) | AT364045B (en) |
| CA (1) | CA1131887A (en) |
| CH (1) | CH635521A5 (en) |
| DE (1) | DE2748159C2 (en) |
| ES (1) | ES474579A1 (en) |
| IL (1) | IL55769A (en) |
| IT (1) | IT1104225B (en) |
| SE (1) | SE429696B (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2948297C2 (en) * | 1978-06-27 | 1985-01-17 | Kraftwerk Union AG, 4330 Mülheim | Nuclear reactor with a liquid coolant |
| DE2828153C3 (en) * | 1978-06-27 | 1984-07-26 | Kraftwerk Union AG, 4330 Mülheim | Nuclear reactor with a liquid coolant |
| US4749505A (en) * | 1985-07-08 | 1988-06-07 | Exxon Chemical Patents Inc. | Olefin polymer viscosity index improver additive useful in oil compositions |
| RU2254626C2 (en) * | 2003-08-21 | 2005-06-20 | Государственное унитарное предприятие Опытное конструкторское бюро машиностроения им. Африкантова И.И. | Steam pressurizer |
| CN109342492B (en) * | 2018-11-23 | 2021-09-10 | 哈尔滨工程大学 | Experimental device and experimental method for researching bubble rupture behavior characteristics of aerosol-containing liquid pool surface |
Citations (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US955004A (en) * | 1909-07-31 | 1910-04-12 | William O Singer | Wrench. |
| US2937981A (en) * | 1951-06-22 | 1960-05-24 | Augustine O Allen | Suppression of water decomposition |
| US3060726A (en) * | 1957-02-07 | 1962-10-30 | Westinghouse Electric Corp | Hydrogen gauge |
| US3113913A (en) * | 1963-12-10 | Sealing and purging system for pressurized water reactor | ||
| US3286992A (en) * | 1965-11-29 | 1966-11-22 | Little Inc A | Mixing device |
| US3353797A (en) * | 1964-07-08 | 1967-11-21 | Sonic Eng Corp | Mixing system |
| US3450388A (en) * | 1968-03-12 | 1969-06-17 | Gen Motors Corp | Mixer with flushing valve in the outlet |
| US3539509A (en) * | 1967-06-08 | 1970-11-10 | Siemens Ag | Method for electromagnetic removal of iron-oxides from liquids |
| US3575294A (en) * | 1967-11-27 | 1971-04-20 | Nippon Rensui Kk | Counterflow, moving bed type, ion exchange apparatus |
| US3663725A (en) * | 1970-04-23 | 1972-05-16 | Gen Electric | Corrosion inhibition |
| US3871842A (en) * | 1971-07-05 | 1975-03-18 | Licentia Gmbh | Exhaust gas cleaning system for handling radioactive fission and activation gases |
| US3964965A (en) * | 1973-01-22 | 1976-06-22 | Siemens Aktiengesellschaft | Pressurized-water reactor coolant gas disposal system |
| US3976541A (en) * | 1974-03-18 | 1976-08-24 | Combustion Engineering, Inc. | Secondary coolant purification system with demineralizer bypass |
| UST955004I4 (en) | 1976-04-05 | 1977-02-01 | Westinghouse Electric Corporation | Method for heat exchanger leak detection in a liquid metal cooled nuclear reactor |
| US4039289A (en) * | 1971-02-08 | 1977-08-02 | Chemsoil Corporation | Sulphur-burning and gaseous products absorption system and components therefor |
| US4043864A (en) * | 1971-12-22 | 1977-08-23 | Kraftwerk Union Aktiengesellschaft | Nuclear power plant having a pressurized-water reactor |
| US4073683A (en) * | 1970-05-19 | 1978-02-14 | Westinghouse Electric Corporation | Boron control system for a nuclear power plant |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3124518A (en) * | 1964-03-10 | Product | ||
| GB694918A (en) * | 1951-02-23 | 1953-07-29 | F S Gibbs Inc | Diffusion of gases in liquids |
| GB1029648A (en) * | 1964-05-22 | 1966-05-18 | Ca Atomic Energy Ltd | Method of suppressing radiolytic water decomposition in nuclear reactors |
| US3944466A (en) * | 1973-07-16 | 1976-03-16 | Westinghouse Electric Corporation | Reducing concentration of gases in nuclear reactor |
| FR2285172A1 (en) * | 1974-09-20 | 1976-04-16 | Commissariat Energie Atomique | Diffusion of hydrogen into pressurised water - using palladium based selectively permeable barrier |
| JPS5141082U (en) * | 1974-09-20 | 1976-03-26 | ||
| CH607934A5 (en) * | 1976-01-27 | 1978-12-15 | Sulzer Ag | Appliance for introducing gases into liquids and/or liquid-solid mixtures |
-
1977
- 1977-10-27 DE DE2748159A patent/DE2748159C2/en not_active Expired
-
1978
- 1978-10-02 US US05/947,671 patent/US4487740A/en not_active Expired - Lifetime
- 1978-10-03 CH CH1024778A patent/CH635521A5/en not_active IP Right Cessation
- 1978-10-05 CA CA312,773A patent/CA1131887A/en not_active Expired
- 1978-10-18 AT AT0748878A patent/AT364045B/en not_active IP Right Cessation
- 1978-10-19 IL IL55769A patent/IL55769A/en unknown
- 1978-10-23 JP JP53129542A patent/JPS5923398B2/en not_active Expired
- 1978-10-24 SE SE7811046A patent/SE429696B/en not_active IP Right Cessation
- 1978-10-26 EP EP78300549A patent/EP0001903B1/en not_active Expired
- 1978-10-26 IT IT09627/78A patent/IT1104225B/en active
- 1978-10-26 ES ES474579A patent/ES474579A1/en not_active Expired
Patent Citations (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3113913A (en) * | 1963-12-10 | Sealing and purging system for pressurized water reactor | ||
| US955004A (en) * | 1909-07-31 | 1910-04-12 | William O Singer | Wrench. |
| US2937981A (en) * | 1951-06-22 | 1960-05-24 | Augustine O Allen | Suppression of water decomposition |
| US3060726A (en) * | 1957-02-07 | 1962-10-30 | Westinghouse Electric Corp | Hydrogen gauge |
| US3353797A (en) * | 1964-07-08 | 1967-11-21 | Sonic Eng Corp | Mixing system |
| US3286992A (en) * | 1965-11-29 | 1966-11-22 | Little Inc A | Mixing device |
| US3539509A (en) * | 1967-06-08 | 1970-11-10 | Siemens Ag | Method for electromagnetic removal of iron-oxides from liquids |
| US3575294A (en) * | 1967-11-27 | 1971-04-20 | Nippon Rensui Kk | Counterflow, moving bed type, ion exchange apparatus |
| US3450388A (en) * | 1968-03-12 | 1969-06-17 | Gen Motors Corp | Mixer with flushing valve in the outlet |
| US3663725A (en) * | 1970-04-23 | 1972-05-16 | Gen Electric | Corrosion inhibition |
| US4073683A (en) * | 1970-05-19 | 1978-02-14 | Westinghouse Electric Corporation | Boron control system for a nuclear power plant |
| US4039289A (en) * | 1971-02-08 | 1977-08-02 | Chemsoil Corporation | Sulphur-burning and gaseous products absorption system and components therefor |
| US3871842A (en) * | 1971-07-05 | 1975-03-18 | Licentia Gmbh | Exhaust gas cleaning system for handling radioactive fission and activation gases |
| US4043864A (en) * | 1971-12-22 | 1977-08-23 | Kraftwerk Union Aktiengesellschaft | Nuclear power plant having a pressurized-water reactor |
| US3964965A (en) * | 1973-01-22 | 1976-06-22 | Siemens Aktiengesellschaft | Pressurized-water reactor coolant gas disposal system |
| US3976541A (en) * | 1974-03-18 | 1976-08-24 | Combustion Engineering, Inc. | Secondary coolant purification system with demineralizer bypass |
| UST955004I4 (en) | 1976-04-05 | 1977-02-01 | Westinghouse Electric Corporation | Method for heat exchanger leak detection in a liquid metal cooled nuclear reactor |
Non-Patent Citations (7)
| Title |
|---|
| Luwa Blendrex Motionless Mixer, (Luwa Corp., date unknown), [hereinafter "Luwa"]. |
| Luwa Blendrex Motionless Mixer, (Luwa Corp., date unknown), hereinafter Luwa . * |
| R. G. Gilbert, et al., Field for Oxygen Transfer and Mixing in Static Mixer Aeration Systems, (Kenics Corp., 1977). * |
| S. J. Chen, KTEK 12345678: The Static Mixer Unit and Principles of Operation, (Kenics Corp., 1972). * |
| S. J. Chen, KTEK-12345678: The Static Mixer Unit and Principles of Operation, (Kenics Corp., 1972). |
| Stata Tube, 12 pp. of Sales Literature for Stata Tube, TAH Industries, 1977 and 1978. * |
| Stata-Tube, 12 pp. of Sales Literature for Stata-Tube, TAH Industries, 1977 and 1978. |
Also Published As
| Publication number | Publication date |
|---|---|
| SE7811046L (en) | 1979-04-28 |
| ES474579A1 (en) | 1979-06-01 |
| SE429696B (en) | 1983-09-19 |
| JPS55453A (en) | 1980-01-05 |
| CA1131887A (en) | 1982-09-21 |
| JPS5923398B2 (en) | 1984-06-01 |
| IT7809627A0 (en) | 1978-10-26 |
| DE2748159C2 (en) | 1984-06-20 |
| IL55769A (en) | 1981-07-31 |
| DE2748159A1 (en) | 1979-05-03 |
| AT364045B (en) | 1981-09-25 |
| IT1104225B (en) | 1985-10-21 |
| EP0001903B1 (en) | 1981-10-21 |
| CH635521A5 (en) | 1983-04-15 |
| ATA748878A (en) | 1981-02-15 |
| EP0001903A1 (en) | 1979-05-16 |
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| AS | Assignment |
Owner name: BABCOCK-BROWN BOVERI REAKTOR GMBH, 6800 MANNHEIM 4 Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNORS:STIEFEL, MAX;WOLFBEIB, ERICH;REEL/FRAME:004305/0618 Effective date: 19780908 |
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